FR2459680A2 - REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE - Google Patents
REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE Download PDFInfo
- Publication number
- FR2459680A2 FR2459680A2 FR8013810A FR8013810A FR2459680A2 FR 2459680 A2 FR2459680 A2 FR 2459680A2 FR 8013810 A FR8013810 A FR 8013810A FR 8013810 A FR8013810 A FR 8013810A FR 2459680 A2 FR2459680 A2 FR 2459680A2
- Authority
- FR
- France
- Prior art keywords
- reactor
- tube
- loop reactor
- hand
- communication
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/04—Separating crystals from mother liquor
- C13B30/14—Dissolving or refining raw sugar
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F21/00—Dissolving
- B01F21/20—Dissolving using flow mixing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/435—Mixing tubes composed of concentric tubular members
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/51—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
- B01F35/833—Flow control by valves, e.g. opening intermittently
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
- B01F35/834—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices the flow of substances to be mixed circulating in a closed circuit, e.g. from a container through valve, driving means, metering means or dispensing means, e.g. 3-way valve, and back to the container
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
- B01J19/2435—Loop-type reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
REACTEUR A BOUCLES POUR REACTIONS CHIMIQUES ET SIMILAIRES. LE REACTEUR A BOUCLES 1 ETANT MONTE HORIZONTALEMENT, UNE TUBULURE DE REMPLISSAGE 8 EST DISPOSEE A LA PARTIE SUPERIEURE DE L'ENVELOPPE ET, EN DEHORS DE L'ENVELOPPE DU REACTEUR, UNE POMPE DE CIRCULATION 11 EST RELIEE AU TUBE DE SORTIE 10, LAQUELLE EST EN COMMUNICATION, PAR L'INTERMEDIAIRE D'UN TUBE 13, D'UNE PART AVEC L'ADMISSION DE LIQUIDE 14 ET, D'AUTRE PART, AVEC LE DISPOSITIF DE SOUTIRAGE 15, 16. UN TEL REACTEUR SE REVELE EFFICACE POUR MELANGER DES SOLIDES AVEC DES LIQUIDES.LOOP REACTOR FOR CHEMICAL AND SIMILAR REACTIONS. THE LOOP REACTOR 1 BEING MOUNTED HORIZONTALLY, A FILLING TUBING 8 IS PROVIDED AT THE UPPER PART OF THE ENCLOSURE AND, OUTSIDE THE REACTOR ENCLOSURE, A CIRCULATION PUMP 11 IS CONNECTED TO THE OUTLET TUBE 10, WHICH IS IN COMMUNICATION, THROUGH A TUBE 13, ON THE ONE HAND WITH THE INLET OF LIQUID 14 AND, ON THE OTHER HAND, WITH THE TAPPING DEVICE 15, 16. SUCH REACTOR IS EFFECTIVE FOR MIXING SOLIDS WITH LIQUIDS.
Description
L'invention est relative à un réacteur à boucles selon le brevet 76 10The invention relates to a loop reactor according to the patent 76 10
888. Des réacteurs de cette structure sont surtout destinés 888. Reactors of this structure are mainly intended for
au mélange des matières liquides.to the mixture of liquid materials.
Les matières solides et liquides,par exemple lors de la prépara- Solids and liquids, for example during the preparation
tion d'une solution de sucre,sont actuellement mélangées dans un dispositif à agitation, Celui-ci consiste le plus souvent en une cuve dans laquelle tourne un agitateur à hélice. Etant donné que, dans ce casles matières solides sont plaquées sur la paroi de la cuve sous l'effet de la force centrifuge,le processus de mélange est long et n'est pas suffisamment intime. Le contenu de la cuve Sugar solution is presently mixed in a stirring device. This is usually a vessel in which a propeller stirrer is rotated. Since in this case the solids are plated on the wall of the tank under the effect of the centrifugal force, the mixing process is long and not sufficiently intimate. The contents of the tank
doit être chaque fois vidé et la cuve être rechargée. Le fonction- must be emptied each time and the tank be recharged. The function
nement discontinu du système d'agitation se traduit,lors de la discontinuous stirring system is reflected, during the
fabrication,par une perte de temps indésirable. manufacturing, by an undesirable waste of time.
Le problème à la base de l'invention est de mettre au point un dispositif dans lequel le mélange de matières solides et liquides The problem underlying the invention is to develop a device in which the mixture of solids and liquids
s'effectue de façon rapide et intense. is done quickly and intensively.
Dans son principele problème est résolu selon l'invention grâce à l'utilisation d'un réacteur à boucles selon le brevet 76 10 888 In its main problem is solved according to the invention through the use of a loop reactor according to the patent 76 10 888
qui s'est déjà révélé extrêmement efficace pour le mélange de matiè- already proven to be extremely effective for the blending of
res liquides. Pour le mélange des matières solides avec des liquides, l'invention fournit un réacteur à boucles comportant une enveloppe de réacteur cylindrique,un tube directeur disposé concentriquement à celleci et muni d'un anneau creux qui est en communicationd'une part,avec l'enceinte de mélange par une ouverture dans l'enveloppe externe du tube directeur et, d'autre part,avec le tube de sortie du réacteur par au moins une autre ouverture à l'extrémité du tube directeur,une admission de liquide disposée concentriquement à l'extrémité opposée du tube directeur et des moyens pour le brassage du liquide selon le brevet 75 10 888,qui présente la particularité liquids. For the mixing of solids with liquids, the invention provides a loop reactor having a cylindrical reactor shell, a steering tube concentrically disposed thereto and provided with a hollow ring which is in communication with both mixing chamber through an opening in the outer casing of the head tube and, secondly, with the reactor outlet tube through at least one other opening at the end of the head tube, a liquid inlet arranged concentrically to the opposite end of the steering tube and means for mixing the liquid according to the patent 75 10 888, which has the particularity
que le réacteur à boucles,étant monté horizontalement,une tubu- that the loop reactor, being mounted horizontally, a tubular
lure de remplissage est disposée à la partie supérieure de l'en- The filling lure is arranged at the top of the enclosure.
veloppe et que,en dehors de l'enveloppe du réacteur,une pompe de veloppe and that, outside the reactor casing, a fuel pump
circulation est reliée au tube de sortielaquelle est en communica- circulation is connected to the output tube which is in communication with
tion,par l'intermédiaire d'un tube,d'une part avec l'admission de tion, through a tube, on the one hand with the admission of
liquide et, d'autre part,avec le dispositif de soutirage. De préfé- liquid and, on the other hand, with the withdrawal device. Preferably
rence,sur la tubulure de remplissage est disposé un indicateur de niveau asservi au dispositif de soutirage. L'invention fournit aussi un procédé de mélange de matières solides avec des liquides qui comporte l'emploi d'un tel réacteur A filling level indicator is provided on the filler neck which is controlled by the draw-off device. The invention also provides a method for mixing solids with liquids which involves the use of such a reactor
à boucles,et selon lequel,de préférence,les matières sont introdui- loops, and according to which, preferably, the materials are introduced
tes en contiru dans le mélange en circulation dans l'enveloppe de réacteur remplie et le mélange est soutiré par pompage,est en partie Contoured in the circulating mixture in the filled reactor casing and the mixture is pumped off, is partly
injecté dans le corps du réacteur et est en partie soutiré. injected into the reactor body and is partially withdrawn.
L'utilisation du réacteur à boucles selon l'invention offre également l'avantage que les matières solides et liquides peuvent The use of the loop reactor according to the invention also has the advantage that solid and liquid materials can
être amenées en continu dans la cuve à réaction. be fed continuously into the reaction vessel.
Le dessin représente une vue latérale,partiellement en coupe, The drawing shows a side view, partially in section,
d'un exemple de réalisation d'un réacteur à boucles selon l'inven- of an embodiment of a loop reactor according to the invention.
tion.tion.
Dans la cuve à réaction cylindrique 1 est logé concentrique- In the cylindrical reaction vessel 1 is housed concentrically
ment le tube directeur 2 qui,sur une partie de sa longueur à double paroi, est constitué par un anneau creux 5 avec une paroi externe 3 et une paroi interne 4,L'extrémité de la paroi externe forme avec la paroi interne une ouverture 6. A l'autre extrémité du tube directeurdes tubes 7 conduisent vers la sortie 10. Sur le bord supérieur de la cuve est disposée une tubulure de remplissage 8, de préférence pour les matières solides,dans laquelle débouche un tube 9 pour liquides. La pompe de circulation 11 également zur la face supérieure de la cuve est en communication avec la sortie 10 par le tube d'aspiration 12 et avec la buse d'injection 14 et la cuve 1 par l'intermédiaire du tube sous pression 13. Le tube de sortie 15,dans lequel est insérée une soupape de réglage 16 couplée à un indicateur de niveau 17 placé dans la tubulure de remplissage 8,est placé en dérivation par rapport au tube sous pression 13, the steering tube 2 which, over part of its double-walled length, is constituted by a hollow ring 5 with an outer wall 3 and an inner wall 4, the end of the outer wall forms with the inner wall an opening 6 At the other end of the tube directing tubes 7 lead to the outlet 10. On the upper edge of the tank is arranged a filling pipe 8, preferably for solids, in which opens a tube 9 for liquids. The circulation pump 11 also on the upper face of the tank is in communication with the outlet 10 via the suction tube 12 and with the injection nozzle 14 and the tank 1 via the pressure tube 13. outlet tube 15, in which is inserted a control valve 16 coupled to a level indicator 17 placed in the filler neck 8, is placed in connection with the pressure tube 13,
Un robinet 18 est destiné à la vidange de la cuve. A valve 18 is intended for emptying the tank.
Le réacteur une fois rempli,la pompe de circulation 11 assure une circulation intense de la quantité de matière chargée à travers le Once the reactor has been filled, the circulation pump 11 ensures an intense circulation of the quantity of material charged through the
réacteur et par conséquent un mélange intime. Aussitôt que le pro- reactor and therefore an intimate mixture. As soon as the
duit fini est soutiré à travers la soupape 16,on règle l'indica- finished product is withdrawn through the valve 16, the indica-
teur de niveau 17 de manière que les produits à mélanger soient level 17 so that the products to be blended are
délivrés vers le réacteur en une quantité correspondant au soutira- delivered to the reactor in an amount corresponding to the
ge du produit fini.ge of the finished product.
Claims (3)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2925191A DE2925191C2 (en) | 1979-06-22 | 1979-06-22 | Loop reactor |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2459680A2 true FR2459680A2 (en) | 1981-01-16 |
FR2459680B2 FR2459680B2 (en) | 1985-04-26 |
Family
ID=6073861
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR8013810A Granted FR2459680A2 (en) | 1979-06-22 | 1980-06-20 | REACTOR WITH BUCKLES FOR CHEMICAL REACTIONS AND THE LIKE |
Country Status (10)
Country | Link |
---|---|
US (1) | US4448539A (en) |
JP (1) | JPS602905B2 (en) |
AT (1) | AT376910B (en) |
BR (1) | BR8003877A (en) |
CH (1) | CH650942A5 (en) |
DE (1) | DE2925191C2 (en) |
FR (1) | FR2459680A2 (en) |
GB (1) | GB2055050B (en) |
IT (1) | IT1147752B (en) |
NL (1) | NL8003552A (en) |
Families Citing this family (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4490049A (en) * | 1983-06-02 | 1984-12-25 | Cron Chemical Corporation | Mixing arrangement |
US4701055A (en) * | 1986-02-07 | 1987-10-20 | Fluid Dynamics, Inc. | Mixing apparatus |
JPH01145301U (en) * | 1988-03-22 | 1989-10-05 | ||
CH682460A5 (en) * | 1990-11-19 | 1993-09-30 | Miteco Ag Angelo Cadeo | Apparatus for dissolving solid bulk material in a liquid. |
GB9101967D0 (en) * | 1991-01-30 | 1991-03-13 | Atomic Energy Authority Uk | Reagent mixing |
IT1253330B (en) * | 1991-07-11 | 1995-07-24 | Agristrade Srl | PHYSICAL DISSOLUTOR |
US5248416A (en) * | 1991-11-18 | 1993-09-28 | Howard Jr Ronnie E | Sewage treatment system |
US5350595A (en) * | 1992-05-13 | 1994-09-27 | Kraft General Foods, Inc. | Method for continuous manufacture of process cheese-type products |
EP0598283B1 (en) * | 1992-11-16 | 1997-10-29 | Bayer Ag | Continuous process for the conversion control of polyurethane prepolymers by partially mixing the prepolymers with monomers |
US5333952A (en) * | 1993-08-17 | 1994-08-02 | Perdue John L | Chemical mixing chamber |
CA2224033A1 (en) * | 1996-12-13 | 1998-06-13 | Kraft Foods, Inc. | Method for continuous manufacture of viscous food products |
US6239235B1 (en) * | 1997-07-15 | 2001-05-29 | Phillips Petroleum Company | High solids slurry polymerization |
ZA991026B (en) * | 1998-02-13 | 2000-08-10 | Coca Cola Co | Continuous dry parts metering and blending system. |
JP3741253B2 (en) * | 1999-12-24 | 2006-02-01 | 富士通株式会社 | Chemical manufacturing equipment |
US6566460B1 (en) | 2000-08-04 | 2003-05-20 | Equistar Chemicals, Lp | Continuous recovery of polymer from a slurry loop reactor |
ES2291668T3 (en) * | 2002-09-23 | 2008-03-01 | Total Petrochemicals Research Feluy | SUSPENSION LOOP POLYOLEFIN REACTOR. |
ES2416314T3 (en) | 2004-08-27 | 2013-07-31 | Chevron Phillips Chemical Company Lp | Polyolefin production processes |
US7629421B2 (en) * | 2005-12-21 | 2009-12-08 | Chevron Phillips Chemical Company Lp | Monomer recovery by returning column overhead liquid to the reactor |
US20090154288A1 (en) * | 2007-12-13 | 2009-06-18 | Heathman James F | On-the-Fly Acid Blender with High-Rate, Single Pass, Emulsification Equipment |
PL2593943T3 (en) * | 2010-07-15 | 2015-03-31 | Mallinckrodt Nuclear Medicine Llc | Slurry dispenser for radioisotope production |
CN104196514B (en) * | 2014-09-02 | 2016-09-14 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | A kind of acidizing and fracturing fluid is i.e. joined and is i.e. used device |
US10252229B2 (en) * | 2017-06-30 | 2019-04-09 | Snowie LLC | System comprising a pump attached to a tank casing for mixing a fluid |
BR102017019628B1 (en) * | 2017-09-14 | 2022-03-29 | Petrobras Transporte S/A - Transpetro | External fluid movement system in a storage tank |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2699379A (en) * | 1949-04-22 | 1955-01-11 | Luque Jose Aramburu | Extraction apparatus |
FR1427464A (en) * | 1964-03-20 | 1966-02-04 | Guenter Strumann | Method and apparatus for dissolving in water or mixing with water aggressive solid or liquid detergents |
US4007921A (en) * | 1976-01-19 | 1977-02-15 | The Dow Chemical Company | Apparatus for mixing dry particles with a liquid |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA130831A (en) * | 1910-10-12 | 1911-01-31 | William C. Paterson | Pulp agitating apparatus |
US2635859A (en) * | 1950-06-12 | 1953-04-21 | Felix W Dreyfus | Mixer apparatus |
US3166020A (en) * | 1961-09-20 | 1965-01-19 | Hypro Engineering Inc | Venturi mixer nozzle |
US3608869A (en) * | 1969-05-28 | 1971-09-28 | Texaco Inc | System for blending liquid ingredients |
DE2232341A1 (en) * | 1972-07-01 | 1974-01-17 | Orthmann & Herbst | Continuous neutralization plant - for acid or alkaline waste water |
US3807700A (en) * | 1972-07-05 | 1974-04-30 | S Kennedy | Mixing apparatus for forming a slurry |
DE2516284C3 (en) * | 1975-04-14 | 1978-04-13 | Burdosa, Herwig Burgert, 6301 Roedgen | Loop reactor |
US4170420A (en) * | 1976-09-13 | 1979-10-09 | Underwood Gene E | Fluid mixing system |
-
1979
- 1979-06-22 DE DE2925191A patent/DE2925191C2/en not_active Expired
-
1980
- 1980-06-12 GB GB8019314A patent/GB2055050B/en not_active Expired
- 1980-06-18 AT AT0323280A patent/AT376910B/en not_active IP Right Cessation
- 1980-06-19 NL NL8003552A patent/NL8003552A/en not_active Application Discontinuation
- 1980-06-20 JP JP55082991A patent/JPS602905B2/en not_active Expired
- 1980-06-20 IT IT67971/80A patent/IT1147752B/en active
- 1980-06-20 BR BR8003877A patent/BR8003877A/en not_active IP Right Cessation
- 1980-06-20 CH CH4775/80A patent/CH650942A5/en not_active IP Right Cessation
- 1980-06-20 FR FR8013810A patent/FR2459680A2/en active Granted
-
1982
- 1982-07-07 US US06/396,041 patent/US4448539A/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2699379A (en) * | 1949-04-22 | 1955-01-11 | Luque Jose Aramburu | Extraction apparatus |
FR1427464A (en) * | 1964-03-20 | 1966-02-04 | Guenter Strumann | Method and apparatus for dissolving in water or mixing with water aggressive solid or liquid detergents |
US4007921A (en) * | 1976-01-19 | 1977-02-15 | The Dow Chemical Company | Apparatus for mixing dry particles with a liquid |
Also Published As
Publication number | Publication date |
---|---|
IT1147752B (en) | 1986-11-26 |
GB2055050B (en) | 1982-12-01 |
US4448539A (en) | 1984-05-15 |
JPS602905B2 (en) | 1985-01-24 |
GB2055050A (en) | 1981-02-25 |
IT8067971A0 (en) | 1980-06-20 |
ATA323280A (en) | 1984-06-15 |
DE2925191C2 (en) | 1982-11-11 |
DE2925191A1 (en) | 1981-03-12 |
FR2459680B2 (en) | 1985-04-26 |
NL8003552A (en) | 1980-12-24 |
CH650942A5 (en) | 1985-08-30 |
JPS5626541A (en) | 1981-03-14 |
AT376910B (en) | 1985-01-25 |
BR8003877A (en) | 1981-01-13 |
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